Mixture of Cyclohexanone + 1,4-Dioxane

Excel

Cyclohexanone

Name
Cyclohexanone
InChI
InChI=1S/C6H10O/c7-6-4-2-1-3-5-6/h1-5H2
InChI Key
JHIVVAPYMSGYDF-UHFFFAOYSA-N
Formula
C6H10O
SMILES
O=C1CCCCC1
Mol. Weight (g/mol)
98.14
CAS
108-94-1

1,4-Dioxane

Name
1,4-Dioxane
InChI
InChI=1S/C4H8O2/c1-2-6-4-3-5-1/h1-4H2
InChI Key
RYHBNJHYFVUHQT-UHFFFAOYSA-N
Formula
C4H8O2
SMILES
C1COCCO1
Mol. Weight (g/mol)
88.11
CAS
123-91-1
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Datasets

  1. Cp,liquid - Molar heat capacity at constant pressure, J/K/mol (2)
  2. η - Viscosity, Pa*s (2)
  3. Excess molar enthalpy (molar enthalpy (2)
  4. ρl - Mass density, kg/m3 (4)
  5. csound,fluid - Speed of Sound, m/s (2)

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
293.15 0.0799 173.61
293.15 0.1351 171.94
293.15 0.1965 170.17
293.15 0.2378 169.01
293.15 0.2874 167.66
293.15 0.3258 166.66
293.15 0.3642 165.66
293.15 0.4195 164.26
293.15 0.4625 163.21
293.15 0.5061 162.15
293.15 0.5543 161.01
293.15 0.6023 159.90
293.15 0.6487 158.83
293.15 0.6946 157.82
293.15 0.7412 156.79
293.15 0.7845 155.87
293.15 0.8398 154.71
293.15 0.8975 153.56
298.15 0.0799 175.65
298.15 0.1351 173.94
298.15 0.1965 172.12
298.15 0.2378 170.93
298.15 0.2874 169.54
298.15 0.3258 168.49
298.15 0.3642 167.46
298.15 0.4195 166.02
298.15 0.4625 164.92
298.15 0.5061 163.82
298.15 0.5543 162.63
298.15 0.6023 161.47
298.15 0.6487 160.36
298.15 0.6946 159.29
298.15 0.7412 158.22
298.15 0.7845 157.25
298.15 0.8398 156.04
298.15 0.8975 154.82
303.15 0.0799 177.71
303.15 0.1351 175.96
303.15 0.1965 174.08
303.15 0.2378 172.86
303.15 0.2874 171.43
303.15 0.3258 170.34
303.15 0.3642 169.27
303.15 0.4195 167.78
303.15 0.4625 166.62
303.15 0.5061 165.49
303.15 0.5543 164.25
303.15 0.6023 163.05
303.15 0.6487 161.90
303.15 0.6946 160.78
303.15 0.7412 159.66
303.15 0.7845 158.66
303.15 0.8398 157.39
303.15 0.8975 156.10
308.15 0.0799 179.75
308.15 0.1351 177.96
308.15 0.1965 176.03
308.15 0.2378 174.77
308.15 0.2874 173.28
308.15 0.3258 172.17
308.15 0.3642 171.07
308.15 0.4195 169.52
308.15 0.4625 168.33
308.15 0.5061 167.15
308.15 0.5543 165.88
308.15 0.6023 164.62
308.15 0.6487 163.44
308.15 0.6946 162.27
308.15 0.7412 161.12
308.15 0.7845 160.06
308.15 0.8398 158.74
308.15 0.8975 157.39

Molar heat capacity at constant pressure, J/K/mol [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Liquid Molar heat capacity at constant pressure, J/K/mol - Liquid
293.15 0.0799 173.61
293.15 0.1351 171.94
293.15 0.1965 170.17
293.15 0.2378 169.01
293.15 0.2874 167.66
293.15 0.3258 166.66
293.15 0.3642 165.66
293.15 0.4195 164.26
293.15 0.4625 163.21
293.15 0.5061 162.15
293.15 0.5543 161.01
293.15 0.6023 159.90
293.15 0.6487 158.83
293.15 0.6946 157.82
293.15 0.7412 156.79
293.15 0.7845 155.87
293.15 0.8398 154.71
293.15 0.8975 153.56
298.15 0.0799 175.65
298.15 0.1351 173.94
298.15 0.1965 172.12
298.15 0.2378 170.93
298.15 0.2874 169.54
298.15 0.3258 168.49
298.15 0.3642 167.46
298.15 0.4195 166.02
298.15 0.4625 164.92
298.15 0.5061 163.82
298.15 0.5543 162.63
298.15 0.6023 161.47
298.15 0.6487 160.36
298.15 0.6946 159.29
298.15 0.7412 158.22
298.15 0.7845 157.25
298.15 0.8398 156.04
298.15 0.8975 154.82
303.15 0.0799 177.71
303.15 0.1351 175.96
303.15 0.1965 174.08
303.15 0.2378 172.86
303.15 0.2874 171.43
303.15 0.3258 170.34
303.15 0.3642 169.27
303.15 0.4195 167.78
303.15 0.4625 166.62
303.15 0.5061 165.49
303.15 0.5543 164.25
303.15 0.6023 163.05
303.15 0.6487 161.90
303.15 0.6946 160.78
303.15 0.7412 159.66
303.15 0.7845 158.66
303.15 0.8398 157.39
303.15 0.8975 156.10
308.15 0.0799 179.75
308.15 0.1351 177.96
308.15 0.1965 176.03
308.15 0.2378 174.77
308.15 0.2874 173.28
308.15 0.3258 172.17
308.15 0.3642 171.07
308.15 0.4195 169.52
308.15 0.4625 168.33
308.15 0.5061 167.15
308.15 0.5543 165.88
308.15 0.6023 164.62
308.15 0.6487 163.44
308.15 0.6946 162.27
308.15 0.7412 161.12
308.15 0.7845 160.06
308.15 0.8398 158.74
308.15 0.8975 157.39

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Cyclohexanone (1) - Liquid Viscosity, Pa*s - Liquid
288.15 0.0990 0.0014
288.15 0.2022 0.0015
288.15 0.3100 0.0015
288.15 0.4227 0.0016
288.15 0.5406 0.0017
288.15 0.6641 0.0019
288.15 0.7280 0.0020
288.15 0.8607 0.0022
288.15 0.9295 0.0024
293.15 0.0990 0.0013
293.15 0.2022 0.0014
293.15 0.3100 0.0014
293.15 0.4227 0.0015
293.15 0.5406 0.0016
293.15 0.6641 0.0017
293.15 0.7280 0.0018
293.15 0.8607 0.0020
293.15 0.9295 0.0021
298.15 0.0990 0.0012
298.15 0.2022 0.0012
298.15 0.3100 0.0013
298.15 0.4227 0.0013
298.15 0.5406 0.0014
298.15 0.6641 0.0015
298.15 0.7280 0.0016
298.15 0.8607 0.0018
298.15 0.9295 0.0019
303.15 0.0990 0.0011
303.15 0.2022 0.0011
303.15 0.3100 0.0012
303.15 0.4227 0.0012
303.15 0.5406 0.0013
303.15 0.6641 0.0014
303.15 0.7280 0.0015
303.15 0.8607 0.0017
303.15 0.9295 0.0018
308.15 0.0990 0.0010
308.15 0.2022 0.0011
308.15 0.3100 0.0011
308.15 0.4227 0.0011
308.15 0.5406 0.0012
308.15 0.6641 0.0013
308.15 0.7280 0.0014
308.15 0.8607 0.0015
308.15 0.9295 0.0016
313.15 0.0990 0.0010
313.15 0.2022 0.0010
313.15 0.3100 0.0010
313.15 0.4227 0.0011
313.15 0.5406 0.0011
313.15 0.6641 0.0012
313.15 0.7280 0.0013
313.15 0.8607 0.0014
313.15 0.9295 0.0015

Viscosity, Pa*s [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Cyclohexanone (1) - Liquid Viscosity, Pa*s - Liquid
288.15 0.0990 0.0014
288.15 0.2022 0.0015
288.15 0.3100 0.0015
288.15 0.4227 0.0016
288.15 0.5406 0.0017
288.15 0.6641 0.0019
288.15 0.7280 0.0020
288.15 0.8607 0.0022
288.15 0.9295 0.0024
293.15 0.0990 0.0013
293.15 0.2022 0.0014
293.15 0.3100 0.0014
293.15 0.4227 0.0015
293.15 0.5406 0.0016
293.15 0.6641 0.0017
293.15 0.7280 0.0018
293.15 0.8607 0.0020
293.15 0.9295 0.0021
298.15 0.0990 0.0012
298.15 0.2022 0.0012
298.15 0.3100 0.0013
298.15 0.4227 0.0013
298.15 0.5406 0.0014
298.15 0.6641 0.0015
298.15 0.7280 0.0016
298.15 0.8607 0.0018
298.15 0.9295 0.0019
303.15 0.0990 0.0011
303.15 0.2022 0.0011
303.15 0.3100 0.0012
303.15 0.4227 0.0012
303.15 0.5406 0.0013
303.15 0.6641 0.0014
303.15 0.7280 0.0015
303.15 0.8607 0.0017
303.15 0.9295 0.0018
308.15 0.0990 0.0010
308.15 0.2022 0.0011
308.15 0.3100 0.0011
308.15 0.4227 0.0011
308.15 0.5406 0.0012
308.15 0.6641 0.0013
308.15 0.7280 0.0014
308.15 0.8607 0.0015
308.15 0.9295 0.0016
313.15 0.0990 0.0010
313.15 0.2022 0.0010
313.15 0.3100 0.0010
313.15 0.4227 0.0011
313.15 0.5406 0.0011
313.15 0.6641 0.0012
313.15 0.7280 0.0013
313.15 0.8607 0.0014
313.15 0.9295 0.0015

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of 1,4-Dioxane (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0792 0.0817
0.1286 0.1245
0.1749 0.1595
0.2236 0.1916
0.2743 0.2201
0.3289 0.2455
0.3729 0.2622
0.4298 0.2787
0.4715 0.2871
0.5242 0.2930
0.5735 0.2935
0.6199 0.2892
0.7182 0.2624
0.7628 0.2412
0.8193 0.2048
0.8672 0.1647
0.9173 0.1125

Excess molar enthalpy (molar enthalpy of mixing), kJ/mol [ref]

Operational conditions:

Mole fraction of 1,4-Dioxane (2) - Liquid Excess molar enthalpy (molar enthalpy of mixing), kJ/mol - Liquid
0.0792 0.0817
0.1286 0.1245
0.1749 0.1595
0.2236 0.1916
0.2743 0.2201
0.3289 0.2455
0.3729 0.2622
0.4298 0.2787
0.4715 0.2871
0.5242 0.2930
0.5735 0.2935
0.6199 0.2892
0.7182 0.2624
0.7628 0.2412
0.8193 0.2048
0.8672 0.1647
0.9173 0.1125

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Cyclohexanone (1) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0990 1027.6
288.15 0.2022 1016.9
288.15 0.3100 1006.5
288.15 0.4227 996.8
288.15 0.5406 986.5
288.15 0.6641 976.8
288.15 0.7280 971.2
288.15 0.8607 962.7
288.15 0.9295 957.7
293.15 0.0990 1021.8
293.15 0.2022 1011.3
293.15 0.3100 1000.8
293.15 0.4227 991.4
293.15 0.5406 981.7
293.15 0.6641 972.0
293.15 0.7280 966.1
293.15 0.8607 958.1
293.15 0.9295 953.1
298.15 0.0990 1016.5
298.15 0.2022 1006.2
298.15 0.3100 996.0
298.15 0.4227 986.4
298.15 0.5406 976.2
298.15 0.6641 966.8
298.15 0.7280 961.4
298.15 0.8607 953.2
298.15 0.9295 948.5
303.15 0.0990 1011.1
303.15 0.2022 1000.9
303.15 0.3100 990.8
303.15 0.4227 981.1
303.15 0.5406 971.5
303.15 0.6641 962.2
303.15 0.7280 956.9
303.15 0.8607 948.8
303.15 0.9295 943.8
308.15 0.0990 1005.5
308.15 0.2022 995.4
308.15 0.3100 985.5
308.15 0.4227 975.2
308.15 0.5406 966.5
308.15 0.6641 957.5
308.15 0.7280 952.4
308.15 0.8607 944.3
308.15 0.9295 939.1
313.15 0.0990 999.9
313.15 0.2022 989.7
313.15 0.3100 979.5
313.15 0.4227 970.7
313.15 0.5406 961.4
313.15 0.6641 952.5
313.15 0.7280 947.2
313.15 0.8607 939.4
313.15 0.9295 934.3

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0999 953.66
293.15 0.1548 957.29
293.15 0.2064 960.83
293.15 0.2523 964.08
293.15 0.3087 968.21
293.15 0.3412 970.67
293.15 0.3952 974.86
293.15 0.4315 977.76
293.15 0.4875 982.38
293.15 0.5348 986.41
293.15 0.5798 990.36
293.15 0.6145 993.49
293.15 0.6698 998.63
293.15 0.7148 1002.9
293.15 0.7682 1008.2
293.15 0.8015 1011.6
293.15 0.8542 1017.2
293.15 0.9054 1022.7
298.15 0.0999 949.13
298.15 0.1548 952.73
298.15 0.2064 956.23
298.15 0.2523 959.45
298.15 0.3087 963.55
298.15 0.3412 965.97
298.15 0.3952 970.12
298.15 0.4315 972.99
298.15 0.4875 977.54
298.15 0.5348 981.52
298.15 0.5798 985.42
298.15 0.6145 988.51
298.15 0.6698 993.56
298.15 0.7148 997.82
298.15 0.7682 1003.0
298.15 0.8015 1006.4
298.15 0.8542 1011.8
298.15 0.9054 1017.3
303.15 0.0999 944.25
303.15 0.1548 947.83
303.15 0.2064 951.32
303.15 0.2523 954.52
303.15 0.3087 958.59
303.15 0.3412 960.99
303.15 0.3952 965.11
303.15 0.4315 967.96
303.15 0.4875 972.47
303.15 0.5348 976.42
303.15 0.5798 980.28
303.15 0.6145 983.33
303.15 0.6698 988.34
303.15 0.7148 992.55
303.15 0.7682 997.69
303.15 0.8015 1001.0
303.15 0.8542 1006.4
303.15 0.9054 1011.7
308.15 0.0999 939.34
308.15 0.1548 942.9
308.15 0.2064 946.37
308.15 0.2523 949.56
308.15 0.3087 953.6
308.15 0.3412 955.99
308.15 0.3952 960.08
308.15 0.4315 962.9
308.15 0.4875 967.38
308.15 0.5348 971.29
308.15 0.5798 975.11
308.15 0.6145 978.13
308.15 0.6698 983.08
308.15 0.7148 987.23
308.15 0.7682 992.32
308.15 0.8015 995.58
308.15 0.8542 1000.8
308.15 0.9054 1006.2

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 101 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of Cyclohexanone (1) - Liquid Mass density, kg/m3 - Liquid
288.15 0.0990 1027.6
288.15 0.2022 1016.9
288.15 0.3100 1006.5
288.15 0.4227 996.8
288.15 0.5406 986.5
288.15 0.6641 976.8
288.15 0.7280 971.2
288.15 0.8607 962.7
288.15 0.9295 957.7
293.15 0.0990 1021.8
293.15 0.2022 1011.3
293.15 0.3100 1000.8
293.15 0.4227 991.4
293.15 0.5406 981.7
293.15 0.6641 972.0
293.15 0.7280 966.1
293.15 0.8607 958.1
293.15 0.9295 953.1
298.15 0.0990 1016.5
298.15 0.2022 1006.2
298.15 0.3100 996.0
298.15 0.4227 986.4
298.15 0.5406 976.2
298.15 0.6641 966.8
298.15 0.7280 961.4
298.15 0.8607 953.2
298.15 0.9295 948.5
303.15 0.0990 1011.1
303.15 0.2022 1000.9
303.15 0.3100 990.8
303.15 0.4227 981.1
303.15 0.5406 971.5
303.15 0.6641 962.2
303.15 0.7280 956.9
303.15 0.8607 948.8
303.15 0.9295 943.8
308.15 0.0990 1005.5
308.15 0.2022 995.4
308.15 0.3100 985.5
308.15 0.4227 975.2
308.15 0.5406 966.5
308.15 0.6641 957.5
308.15 0.7280 952.4
308.15 0.8607 944.3
308.15 0.9295 939.1
313.15 0.0990 999.9
313.15 0.2022 989.7
313.15 0.3100 979.5
313.15 0.4227 970.7
313.15 0.5406 961.4
313.15 0.6641 952.5
313.15 0.7280 947.2
313.15 0.8607 939.4
313.15 0.9295 934.3

Mass density, kg/m3 [ref]

Operational condition: Pressure, kPa = 100 (Liquid)

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Liquid Mass density, kg/m3 - Liquid
293.15 0.0999 953.66
293.15 0.1548 957.29
293.15 0.2064 960.83
293.15 0.2523 964.08
293.15 0.3087 968.21
293.15 0.3412 970.67
293.15 0.3952 974.86
293.15 0.4315 977.76
293.15 0.4875 982.38
293.15 0.5348 986.41
293.15 0.5798 990.36
293.15 0.6145 993.49
293.15 0.6698 998.63
293.15 0.7148 1002.9
293.15 0.7682 1008.2
293.15 0.8015 1011.6
293.15 0.8542 1017.2
293.15 0.9054 1022.7
298.15 0.0999 949.13
298.15 0.1548 952.73
298.15 0.2064 956.23
298.15 0.2523 959.45
298.15 0.3087 963.55
298.15 0.3412 965.97
298.15 0.3952 970.12
298.15 0.4315 972.99
298.15 0.4875 977.54
298.15 0.5348 981.52
298.15 0.5798 985.42
298.15 0.6145 988.51
298.15 0.6698 993.56
298.15 0.7148 997.82
298.15 0.7682 1003.0
298.15 0.8015 1006.4
298.15 0.8542 1011.8
298.15 0.9054 1017.3
303.15 0.0999 944.25
303.15 0.1548 947.83
303.15 0.2064 951.32
303.15 0.2523 954.52
303.15 0.3087 958.59
303.15 0.3412 960.99
303.15 0.3952 965.11
303.15 0.4315 967.96
303.15 0.4875 972.47
303.15 0.5348 976.42
303.15 0.5798 980.28
303.15 0.6145 983.33
303.15 0.6698 988.34
303.15 0.7148 992.55
303.15 0.7682 997.69
303.15 0.8015 1001.0
303.15 0.8542 1006.4
303.15 0.9054 1011.7
308.15 0.0999 939.34
308.15 0.1548 942.9
308.15 0.2064 946.37
308.15 0.2523 949.56
308.15 0.3087 953.6
308.15 0.3412 955.99
308.15 0.3952 960.08
308.15 0.4315 962.9
308.15 0.4875 967.38
308.15 0.5348 971.29
308.15 0.5798 975.11
308.15 0.6145 978.13
308.15 0.6698 983.08
308.15 0.7148 987.23
308.15 0.7682 992.32
308.15 0.8015 995.58
308.15 0.8542 1000.8
308.15 0.9054 1006.2

Speed of sound, m/s [ref]

Operational conditions:

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Liquid Speed of sound, m/s - Liquid
293.15 0.0999 1423.2
293.15 0.1548 1419.0
293.15 0.2064 1415.2
293.15 0.2523 1411.8
293.15 0.3087 1407.8
293.15 0.3412 1405.5
293.15 0.3952 1401.8
293.15 0.4315 1399.3
293.15 0.4875 1395.6
293.15 0.5348 1392.5
293.15 0.5798 1389.7
293.15 0.6145 1387.5
293.15 0.6698 1384.1
293.15 0.7148 1381.5
293.15 0.7682 1378.5
293.15 0.8015 1376.8
293.15 0.8542 1374.1
293.15 0.9054 1371.7
298.15 0.0999 1407.2
298.15 0.1548 1402.8
298.15 0.2064 1398.7
298.15 0.2523 1395.1
298.15 0.3087 1390.8
298.15 0.3412 1388.3
298.15 0.3952 1384.3
298.15 0.4315 1381.6
298.15 0.4875 1377.6
298.15 0.5348 1374.2
298.15 0.5798 1371.1
298.15 0.6145 1368.7
298.15 0.6698 1365.0
298.15 0.7148 1362.0
298.15 0.7682 1358.7
298.15 0.8015 1356.7
298.15 0.8542 1353.6
298.15 0.9054 1350.8
303.15 0.0999 1387.0
303.15 0.1548 1382.6
303.15 0.2064 1378.5
303.15 0.2523 1374.9
303.15 0.3087 1370.6
303.15 0.3412 1368.1
303.15 0.3952 1364.0
303.15 0.4315 1361.3
303.15 0.4875 1357.2
303.15 0.5348 1353.8
303.15 0.5798 1350.6
303.15 0.6145 1348.2
303.15 0.6698 1344.4
303.15 0.7148 1341.4
303.15 0.7682 1338.0
303.15 0.8015 1335.9
303.15 0.8542 1332.7
303.15 0.9054 1329.6
308.15 0.0999 1367.1
308.15 0.1548 1362.7
308.15 0.2064 1358.7
308.15 0.2523 1355.0
308.15 0.3087 1350.6
308.15 0.3412 1348.1
308.15 0.3952 1343.9
308.15 0.4315 1341.2
308.15 0.4875 1336.9
308.15 0.5348 1333.5
308.15 0.5798 1330.2
308.15 0.6145 1327.7
308.15 0.6698 1323.8
308.15 0.7148 1320.7
308.15 0.7682 1317.1
308.15 0.8015 1314.9
308.15 0.8542 1311.5
308.15 0.9054 1308.3

Speed of sound, m/s [ref]

Operational conditions:

Fixed Measured
Temperature, K - Liquid Mole fraction of 1,4-Dioxane (2) - Liquid Speed of sound, m/s - Liquid
293.15 0.0999 1423.2
293.15 0.1548 1419.0
293.15 0.2064 1415.2
293.15 0.2523 1411.8
293.15 0.3087 1407.8
293.15 0.3412 1405.5
293.15 0.3952 1401.8
293.15 0.4315 1399.3
293.15 0.4875 1395.6
293.15 0.5348 1392.5
293.15 0.5798 1389.7
293.15 0.6145 1387.5
293.15 0.6698 1384.1
293.15 0.7148 1381.5
293.15 0.7682 1378.5
293.15 0.8015 1376.8
293.15 0.8542 1374.1
293.15 0.9054 1371.7
298.15 0.0999 1407.2
298.15 0.1548 1402.8
298.15 0.2064 1398.7
298.15 0.2523 1395.1
298.15 0.3087 1390.8
298.15 0.3412 1388.3
298.15 0.3952 1384.3
298.15 0.4315 1381.6
298.15 0.4875 1377.6
298.15 0.5348 1374.2
298.15 0.5798 1371.1
298.15 0.6145 1368.7
298.15 0.6698 1365.0
298.15 0.7148 1362.0
298.15 0.7682 1358.7
298.15 0.8015 1356.7
298.15 0.8542 1353.6
298.15 0.9054 1350.8
303.15 0.0999 1387.0
303.15 0.1548 1382.6
303.15 0.2064 1378.5
303.15 0.2523 1374.9
303.15 0.3087 1370.6
303.15 0.3412 1368.1
303.15 0.3952 1364.0
303.15 0.4315 1361.3
303.15 0.4875 1357.2
303.15 0.5348 1353.8
303.15 0.5798 1350.6
303.15 0.6145 1348.2
303.15 0.6698 1344.4
303.15 0.7148 1341.4
303.15 0.7682 1338.0
303.15 0.8015 1335.9
303.15 0.8542 1332.7
303.15 0.9054 1329.6
308.15 0.0999 1367.1
308.15 0.1548 1362.7
308.15 0.2064 1358.7
308.15 0.2523 1355.0
308.15 0.3087 1350.6
308.15 0.3412 1348.1
308.15 0.3952 1343.9
308.15 0.4315 1341.2
308.15 0.4875 1336.9
308.15 0.5348 1333.5
308.15 0.5798 1330.2
308.15 0.6145 1327.7
308.15 0.6698 1323.8
308.15 0.7148 1320.7
308.15 0.7682 1317.1
308.15 0.8015 1314.9
308.15 0.8542 1311.5
308.15 0.9054 1308.3

Sources